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US2789772A - Process and apparatus for forming clay slip - Google Patents

Process and apparatus for forming clay slip Download PDF

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US2789772A
US2789772A US378051A US37805153A US2789772A US 2789772 A US2789772 A US 2789772A US 378051 A US378051 A US 378051A US 37805153 A US37805153 A US 37805153A US 2789772 A US2789772 A US 2789772A
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chamber
clay
slip
blades
upright
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US378051A
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John T Williamson
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Thiele Kaolin Co
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Thiele Kaolin Co
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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B02CRUSHING, PULVERISING, OR DISINTEGRATING; PREPARATORY TREATMENT OF GRAIN FOR MILLING
    • B02CCRUSHING, PULVERISING, OR DISINTEGRATING IN GENERAL; MILLING GRAIN
    • B02C18/00Disintegrating by knives or other cutting or tearing members which chop material into fragments
    • B02C18/06Disintegrating by knives or other cutting or tearing members which chop material into fragments with rotating knives
    • B02C18/08Disintegrating by knives or other cutting or tearing members which chop material into fragments with rotating knives within vertical containers
    • B02C18/12Disintegrating by knives or other cutting or tearing members which chop material into fragments with rotating knives within vertical containers with drive arranged below container

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  • This invention relates to a process and apparatus for forming clay slip and more particularly to the formation of clay slip directly at, and as a part of, the mining operation.
  • clay In the United States, clay, and particularly tine china clay, occurs under a consideral overburden of other material or of clay which is unsuitable for treatment. For this and other reasons, it has beenthe practice heretofore to mine the clay by customary excavation processes, transport the clay by truck to a central processing area at some distance from the mine, after which it iS then stored in a storage heap for future use. At some time after storage, the clay is removed again to a blunging mill and formed into a slip by conventional blunging processes.
  • Another advantage of the present process is that not only does the present disintegrator operate at a capacity from 2 to 4 times that of known clay blungers, but it will produce a clay slip with as much as 50% less water in such fluidity that it can be transmitted by pipeline for long distances without settling.
  • a counterflow disintegrator including as its essential disintegrating element disintegrating knives and particularly knives arranged to provide a shaving or paring action.
  • the unit has a smooth bottom formed of metal plates reinforced by longitudinal stringers so that it may be readily moved from place to place in a mine along with a drag line which is used for removing the overburden and also for charging the disintegrator with crude clay.
  • the entire operation is extremely flexible.
  • Fig. 1 is a side elevation of the apparatus of the invention
  • Fig. 2 is a top plan view thereof, with a portion broken away to show the motor mounting;
  • Fig. 3 is a fragmentary vertical central sectional view of the apparatus on an enlarged scale, the disintegrator head being shown in elevation;
  • Fig. 4 is a vertical central sectional view ofthe disintegrator mechanism
  • Fig. 5 is a plan view of the disintegrator head on a reduced scale
  • iFig. 6 is a fragmentary sectional view taken as indicated along the line 6-6 of Fig. 1; andl p 2,789,772 Patented Apr'. 23 1957 Y Fig. 7 is a fragmentary elevational generally schematic view of the screen shown in Fig. 6.
  • the apparatus of the invention includes a base frame, indicated generally at 8, having three longitudinal stringers 9 sheathed by top sheet metal 'plates forming a Hoor 10 and bottom plates forming a sled surface 11, upon which it may be moved from place to place in a clay pit.
  • the blunger unit 13 has a cylindrical outer shell 15 which is formed of sheet metal, and in the top of the shell 15 is aclay feed hopper 16 through which uncrushed crude clay may be fed into a blunger chamber 17 which occupies the lower part of the shell 15.
  • a disintegrator unit indicated generally at 18.
  • a supporting casing 19 At the lower end of the blunger unit 13, below the disintegrator unit 18 is a supporting casing 19 which has a frusto-conical bottom portion 20 alfording a support for a vertical spindle 21 of the disintegrator 18.
  • the spindle 21 beneath ⁇ the spindle support 20 the spindle 21 is provided with a large driven pulley 22 lby means of which the spindle may be connected to a drive pulley 23 of an electric motor 24 through multiple V drive belts 25.
  • An idler pulley 26 is mounted beneath the supporting frame 19 to prevent the drive belts 25 from running off the pulleys.
  • the drive belts 25 may be adjusted in any desired manner, and as a specific example of a mechanism ⁇ for adjusting the belt tension, the motor 24 is shown in Fig. 2 as being mounted upon a hinged base plate 27 which is secured to a supporting plate 28 which is carried on legs 29 anchored to the blunger shell, there being a suitable retaining member 30 for holding the hinged plate 27 in any desired adjusted ⁇ position in relation to the plate 28.
  • the motor 24 is a 100 H. P. motor which operates at 1160 R. P. M..
  • the pulley 23 is preferably 13 inches in diameter and the pulley 22 is 50 inches in diameter so that the disintegrator head 18 rotates at approximately 300 R. P. M.
  • a mixture of water and a dispel-sing agent for forming a clay slip may enter the blunger chamber 17 through an inlet pipe 31, the dispersing agent being introduced into the pipe 31 through a chemical line 32 which communicates with a tank containing a supply of chemical.
  • the chemical supply is remote from the portable unit and flows through a rubber hose; although it is obvious that a chemical tank could be mounted adjacent the blunger unit 13.
  • the water inlet pipe 31 extends beneath :the blunger unit and has connected thereto, a rubber hose 33 (see Fig. 2) which is coupled to a pressure water system.
  • the disintegrator unit 18 has its shaft 21 supported in a suitable roller bearing assembly 34 which is mounted in the base of the spindle support 2t) in the bottom of the blunger unit 13 and has its lower end supported in a thrust bearing 34a on the floor 10.
  • the upper portion of the shaft 21 passes through a stuffing box 35 which is bolted to a central supporting frame 36 which forms the inside wall of the blunger chamber 17.
  • the stuiiing box 35 has a ber bearing 37 and a packing 3S between which is a fitting 39 which receives a water line 40 which connects with a water seal pump 41 in a water line 42 communicating with the water supply hose 33 (see Fig. 2).
  • a disintegrator head 43 Keyed to the upper end of the shaft 21 above the stuffing box 35 is a disintegrator head 43 which is retained in place on the shaft by means of a head cap 44 which receives a bolt 45.
  • the disintegrator"'head'43 ' hasaflaringskirtd to receive a mounting ring 47 on which are four radially extending cutter arms 43.
  • Each of the arms 48 has a beveled lforward edge49'which serves as a web blade, and at the end of each of the arms 48 is an upright peripheral blade Sii having an inwardly beveled forward edge'51 .providing a cutting edge which. produces a lathe-like shaving, or paring action on the clay which it contacts.
  • Eachof the upright blades 50 is turned diagonally inwardly with re Spect to a line tangent to the end of the arm 48 at an angle of 8 to said tangent line.
  • the angular disposition of the upright blades Si! is of considerable importance in producing the desired agitation, and the paring type of cutting action.
  • The-webblades 49 vare disposed at an angle of 120 'to the upright blades S0, and ⁇ have their adjacent ends somewhat to the rear of the forward sharpened edges of said upright blades.
  • the web ⁇ blades 49 are mounted about one-fourth of -thedistance vup the upright blades th. VIn a disintegratorhead 40 inches in diameter, 6 inch vertical blades% inch-thick have proved satisfactory, and the web blades are approximately 4 inc-hes wide at the outside and Sinches wide at the inside portions.
  • the web blades are preferably bolted to the ring-47 so that they may be replaced when necessary.
  • the -40 inch diameter of the disintegrating head 18 ' is important in combination with the 3G() R. P. M. rate of rotation of the disintegrator head.
  • va Vperipheral discharge Weir 52 which is separated lfrom the blunger chamber by a perforated screen 53 supported by posts Elia-and the weir has an inclined outletd which communicates with a surgetank 55.
  • the screen 53 has 1A; inch openings on Mi inch centers.
  • a discharge pipe 56 which communicates with a centrifugal pump .57 for pumping the slip to any desired location for storage or further processing. Since the apparatus is portable, the discharge side of the lpump yScommunicates with a rubber hose SS.
  • the pump has a drive shaft 59 provided with a pulley 6@ by means of which the-.pump is driven from a motor 61 through a belt 62 which is trained over the pulley 60 and a motor pulley 63.
  • the pump motori is-a 40 H. P. motor which .operatesat 1,750 R. P. .M.
  • the water supply hose 33 and the slip discharge hose 58 are suitably 65/sinches outside diameter.
  • ⁇ Power for operating the motors 2d and 61 and auxi- :liary power is derived through an electric conduit cable 64 which may conveniently be a standard 200 ampere, 259 strand, three conductor, portable mine cable.
  • the apparatus may be open on the sides, as shown, or may conveniently be enclosed by appropriate panels around its side walls, some of which are stationary and vsome of which are hinged to provide access to various parts of the mechanism.
  • a ladder 65 is mounted at one end of ⁇ theframe i2.
  • a suitable drain valve 6e is provided which may be controlled by a handle 67 below the blunger chamber.
  • clay is fed into the blunger chamber i7 from above through the hopper i6 at a controlled rate by means of a drag line unit or other suitable material moving mechanism.
  • Water and a suitable dispersing agent are introduced into the blunger chamber i7 through the water pipe 31 and the communicating chemical line 32, the mixture of water and chemical flowing upwardly into the blunger chamber .i7 from below the level of the disintegrator head 18.
  • the yclay need not be crushed prior to being fed into the blun'ger chamber 17, and this eliminates one'foperation whichis -essential in usual clay processing.
  • pinheads'of clay in the'slip are normally only about 1% of the solids, which is less than in other types of 'blungers
  • Coarse non-clay impurities may occasionally run as ⁇ high as 'l0-15%.
  • the lpinheads and coarse impurities areflate'r removed from theslip in a sand classifier.
  • the relatively la'rge screen openings ⁇ serve to prevent any 'large build-up'of impurities, such as sand and quartz, in the' blunger chamber.
  • 'Apparatus for forming clay slip comprising: a chamber; means for feeding clay'into said chamber; means Vfor feeding water into said chamber; means for feeding a dispersing agent ⁇ into-*said chamber; a rapidly rotatable headY in said .chamber having a .plurality -of cutter arms, eachof said arms vhavingA a generally horizontally disposed 'cuttingblade with a sharpened forward edge and an uprightl bladefat its -end which is disposed at a small angle Ttoa-line tangent to theiend -of'the arm, said upright blade havinga sharpened forward edgewhich lies inside said line; ⁇ and means for withdrawing clay slip from the top ⁇ ofsaid chamber.
  • Apparatus for forming clay slip comprising: a chamber; a hopper-'through -whichfraw -clay may ⁇ be fed into said chamber fromfaboveya conduit for feeding water .and a dispersing agent into-said chamber from below;
  • a :head -onsaid spindle having a plurality of arms each of which has a generallyhorizontally disposed web blade :and an-.u'prightvblade at itslend, said-*blades having sharpenedfforward edges; a peripheral disposed, foraminous screen at the top of the chamber to .permit the passage l ⁇ only fof clay ⁇ particles smaller than ⁇ a predetermined size;
  • a disintegrator head assembly having a Iplurality of horizontally disposed cutting arms provided with blades having forwardly facingshearing type cutting edges, upright blades placed at the outer end of said arms which are inclined with their forward end inwardly from a line tangent to the end of the arm.
  • Apparatus for forming a clay slip comprising a chamber, a hopper above said chamber through which raw clay may be fed into the chamber, -means for feeding water into the chamber from below, means for feeding a dispersing agent into the chamber, an upright rapidly rotatable spindle in said chamber, drive means for the spindle, a head on said spindle having a plurality of arms having generally horizontally disposed blades and upright cutting blades at the end thereof, a foraminous screen at the top of the chamber to permit the passage only of clay particles smaller than a predetermined size; and a discharge Weir surrounding said screen whereby said apparatus may operate continuously with only dispersed clay slip discharging into said weir.
  • Apparatus for forming clay slip comprising: a chamber; means through which raw clay may be fed into said chamber, means through which a counter ow of water may be fed into said chamber, and means through which a dispersing agent may be fed into said chamber; a rapidly rotatable head adapted to rotate about its vertical axis in saidchamber having a plurality of cutter arms provided with blades having forwardly facing cutting edges so that when said head is rotated the mixture is violently agitated with a vortex action and the clay is subjected to a shearing type of cutting action, each of said cutter arms having a horizontally disposed cutting blade and a straight upright blade at its outer end which is inclined with its forward cutting edge inwardly from a line tangent to the end of said arms; and means for withdrawing clay slip from the top of said chamber.
  • the apparatus for forming clap slip comprising: a chamber; means through which raw clay may be fed into said chamber, means through which a counter-flow of water may be fed into said chamber, and means through which a dispersing agent may be fed into said chamber; a rapidly rotatable head adapted to rotate about its vertical axis in said chamber having a plurality of cutter arms provided with blades having forwardly facing cutting edges so that when said head is rotated the mixture is violently agitated with a vortex action and the clay is subjected to a shearing type of action, each of said cutter arms having an upright blade at its outerend, said upright blades being inclined with their forward cutting edge inwardly from a line tangent to the end of the arms; and means for withdrawing clay slip from the top of said chamber.
  • a disintegrator head assembly having a plurality of cutter arms provided with blades having forwardly facing cutting edges, said cutter arms having a horizontally disposed forward cutting blade and an upright blade at its outer end, said upright blade being inclined with its forward cutting edge inwardly from a line tangent to the end of said arms.

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Description

April 23, 1957 J. T. WILLIAMSON PRocEss ANDA APPARATUS FOR FORMING CLAY SLIP Filed sept. 2, 1953 f 5 Sheets-Sheet l .fia
INVENTOR. ET/)/anwo/Z BY SMQ-w@ MM;
Apri-l 23, 1957 J. T. WILLIAMSON PROCESS AND APPARATUS FOR FORMING CLAY SLIP 3 Sheets-Sheet 2 Filed Sept. 2. 1953 IN VEN TOR NJ/(dwl J5/272 Nida/725.072, BY J April 23. 1957 J. T. WILLIAMSON 2,789,772
` PROCESS AND APPARATUS FOR FORMING'CLAY SLIP Filed Sept. 2, 1953 3 Sheets-Sheet 3 IN V EN TOR.
PROCESS AND APPARATUS FOR FORMIN CLAY SLIP John T. Williamson, Sandersville, Ga., assignor to Thiele Kaolin Company, Sandersville, Ga., a corporation of Georgia Application September 2, 1953, Serial No. 378,051
16 Claims. (Cl. 241-46) This invention relates to a process and apparatus for forming clay slip and more particularly to the formation of clay slip directly at, and as a part of, the mining operation.
In the United States, clay, and particularly tine china clay, occurs under a consideral overburden of other material or of clay which is unsuitable for treatment. For this and other reasons, it has beenthe practice heretofore to mine the clay by customary excavation processes, transport the clay by truck to a central processing area at some distance from the mine, after which it iS then stored in a storage heap for future use. At some time after storage, the clay is removed again to a blunging mill and formed into a slip by conventional blunging processes.
By means of the present process and apparatus, it is ited States Patent() possible to eliminate several of the costly steps here- .p
tofore practiced and to establish a portable claydisintegrator at or in the clay mine itself and to disintegrate the raw clay at comparatively high rates of speed.
Another advantage of the present process is that not only does the present disintegrator operate at a capacity from 2 to 4 times that of known clay blungers, but it will produce a clay slip with as much as 50% less water in such fluidity that it can be transmitted by pipeline for long distances without settling.
In order to accomplish this, I have provided a counterflow disintegrator including as its essential disintegrating element disintegrating knives and particularly knives arranged to provide a shaving or paring action.
The counterflow of water and clay into the blunger, in combination with the rapidly ro-tating disintegrating element which has the disintegratng knives mounted at its periphery, produces .a violent vortex action during which uncrushed crude clay may be thoroughly mixed with water and chemicals at a high rate of speed in a continuous operation. The unit has a smooth bottom formed of metal plates reinforced by longitudinal stringers so that it may be readily moved from place to place in a mine along with a drag line which is used for removing the overburden and also for charging the disintegrator with crude clay. Thus, the entire operation is extremely flexible.
The invention is illustrated in a preferred embodiment in the accompanying drawings in which:y
Fig. 1 is a side elevation of the apparatus of the invention;
Fig. 2 is a top plan view thereof, with a portion broken away to show the motor mounting;
Fig. 3 is a fragmentary vertical central sectional view of the apparatus on an enlarged scale, the disintegrator head being shown in elevation;
Fig. 4 is a vertical central sectional view ofthe disintegrator mechanism;
Fig. 5 is a plan view of the disintegrator head on a reduced scale;
iFig. 6 is a fragmentary sectional view taken as indicated along the line 6-6 of Fig. 1; andl p 2,789,772 Patented Apr'. 23 1957 Y Fig. 7 is a fragmentary elevational generally schematic view of the screen shown in Fig. 6.
'Referring to the draw-ings in greater detail, and referring first to Figs. l and 2, the apparatus of the invention includes a base frame, indicated generally at 8, having three longitudinal stringers 9 sheathed by top sheet metal 'plates forming a Hoor 10 and bottom plates forming a sled surface 11, upon which it may be moved from place to place in a clay pit. An upright frame, indicated generally at 12, surrounds a blunger unit, indicated generally at 13, which is supported on legs 14.
As best seen in Fig. 3, the blunger unit 13 has a cylindrical outer shell 15 which is formed of sheet metal, and in the top of the shell 15 is aclay feed hopper 16 through which uncrushed crude clay may be fed into a blunger chamber 17 which occupies the lower part of the shell 15. Within the blunger chamber 17 is a disintegrator unit, indicated generally at 18. At the lower end of the blunger unit 13, below the disintegrator unit 18 is a supporting casing 19 which has a frusto-conical bottom portion 20 alfording a support for a vertical spindle 21 of the disintegrator 18. Referring .again to Fig. 1, beneath `the spindle support 20 the spindle 21 is provided with a large driven pulley 22 lby means of which the spindle may be connected to a drive pulley 23 of an electric motor 24 through multiple V drive belts 25. An idler pulley 26 is mounted beneath the supporting frame 19 to prevent the drive belts 25 from running off the pulleys.
The drive belts 25 may be adjusted in any desired manner, and as a specific example of a mechanism `for adjusting the belt tension, the motor 24 is shown in Fig. 2 as being mounted upon a hinged base plate 27 which is secured to a supporting plate 28 which is carried on legs 29 anchored to the blunger shell, there being a suitable retaining member 30 for holding the hinged plate 27 in any desired adjusted `position in relation to the plate 28.
The motor 24 is a 100 H. P. motor which operates at 1160 R. P. M.. The pulley 23 is preferably 13 inches in diameter and the pulley 22 is 50 inches in diameter so that the disintegrator head 18 rotates at approximately 300 R. P. M.
A mixture of water and a dispel-sing agent for forming a clay slip may enter the blunger chamber 17 through an inlet pipe 31, the dispersing agent being introduced into the pipe 31 through a chemical line 32 which communicates with a tank containing a supply of chemical. In the illustrated embodiment the chemical supply is remote from the portable unit and flows through a rubber hose; although it is obvious that a chemical tank could be mounted adjacent the blunger unit 13. The water inlet pipe 31 extends beneath :the blunger unit and has connected thereto, a rubber hose 33 (see Fig. 2) which is coupled to a pressure water system.
Referring next to Fig. 4, the disintegrator unit 18 has its shaft 21 supported in a suitable roller bearing assembly 34 which is mounted in the base of the spindle support 2t) in the bottom of the blunger unit 13 and has its lower end supported in a thrust bearing 34a on the floor 10. The upper portion of the shaft 21 passes through a stuffing box 35 which is bolted to a central supporting frame 36 which forms the inside wall of the blunger chamber 17. The stuiiing box 35 has a ber bearing 37 and a packing 3S between which is a fitting 39 which receives a water line 40 which connects with a water seal pump 41 in a water line 42 communicating with the water supply hose 33 (see Fig. 2).
Keyed to the upper end of the shaft 21 above the stuffing box 35 is a disintegrator head 43 which is retained in place on the shaft by means of a head cap 44 which receives a bolt 45.
Referring particularly to Figs. 4 and 5, the disintegrator"'head'43 'hasaflaringskirtd to receive a mounting ring 47 on which are four radially extending cutter arms 43. Each of the arms 48 has a beveled lforward edge49'which serves as a web blade, and at the end of each of the arms 48 is an upright peripheral blade Sii having an inwardly beveled forward edge'51 .providing a cutting edge which. produces a lathe-like shaving, or paring action on the clay which it contacts. Eachof the upright blades 50 is turned diagonally inwardly with re Spect to a line tangent to the end of the arm 48 at an angle of 8 to said tangent line. The angular disposition of the upright blades Si! is of considerable importance in producing the desired agitation, and the paring type of cutting action. The-webblades 49 vare disposed at an angle of 120 'to the upright blades S0, and `have their adjacent ends somewhat to the rear of the forward sharpened edges of said upright blades. The web `blades 49 are mounted about one-fourth of -thedistance vup the upright blades th. VIn a disintegratorhead 40 inches in diameter, 6 inch vertical blades% inch-thick have proved satisfactory, and the web blades are approximately 4 inc-hes wide at the outside and Sinches wide at the inside portions. The web blades are preferably bolted to the ring-47 so that they may be replaced when necessary. The -40 inch diameter of the disintegrating head 18 'is important in combination with the 3G() R. P. M. rate of rotation of the disintegrator head.
As best seen in Fig. 3, at the upper end of the blunger chamber 17 is va Vperipheral discharge Weir 52 which is separated lfrom the blunger chamber by a perforated screen 53 supported by posts Elia-and the weir has an inclined outletd which communicates with a surgetank 55. The screen 53 has 1A; inch openings on Mi inch centers. At the lower end of the surge tank is a discharge pipe 56 which communicates with a centrifugal pump .57 for pumping the slip to any desired location for storage or further processing. Since the apparatus is portable, the discharge side of the lpump yScommunicates with a rubber hose SS. The pump has a drive shaft 59 provided with a pulley 6@ by means of which the-.pump is driven from a motor 61 through a belt 62 which is trained over the pulley 60 and a motor pulley 63. The pump motori is-a 40 H. P. motor which .operatesat 1,750 R. P. .M.
The water supply hose 33 and the slip discharge hose 58 are suitably 65/sinches outside diameter.
`Power for operating the motors 2d and 61 and auxi- :liary power is derived through an electric conduit cable 64 which may conveniently be a standard 200 ampere, 259 strand, three conductor, portable mine cable.
The apparatus may be open on the sides, as shown, or may conveniently be enclosed by appropriate panels around its side walls, some of which are stationary and vsome of which are hinged to provide access to various parts of the mechanism. A ladder 65 is mounted at one end of `theframe i2.
For convenience in draining and cleaning the blunger chamber i7, or when it is necessary to work on the disintegrator mechanism within the chamber, a suitable drain valve 6e is provided which may be controlled by a handle 67 below the blunger chamber.
When the device is in operation clay is fed into the blunger chamber i7 from above through the hopper i6 at a controlled rate by means of a drag line unit or other suitable material moving mechanism. Water and a suitable dispersing agent are introduced into the blunger chamber i7 through the water pipe 31 and the communicating chemical line 32, the mixture of water and chemical flowing upwardly into the blunger chamber .i7 from below the level of the disintegrator head 18. The
,pH of the slip is checked continuously by means of a standard pH control installed in the discharge vfrom the Weir-52, and the-desired-pI-I of the slip is obtained by controlling the flow of chemical through Vthe line 52 in the customary manner. The pH is controlled at the minimum level which will completely' disperse the clay,
which varies with the particular clay being processed.
By reason of the violent vortex action combined with the lathe-like shaving or paring action of the knives on the disintegrator head 1 8, the yclay need not be crushed prior to being fed into the blun'ger chamber 17, and this eliminates one'foperation whichis -essential in usual clay processing.
The mixture of broken clay, water and chemical which .ismoved to the't'op' of Vthe blunger chamber 13 is still in 'rather violent swirling motion, and washes against the screen 53 almost parallel to the surface thereof. In spite of thetfactthatthefholeslin the screen are rather large- 1/s inch on 1A inch centersthe washing action across the screen, combined'witha rolling vortex action in the blunger chamber, tends to permit only very finely divided clay particles to pass through to the weir, while the heavier 'particles aresucked back toward the center and again pass through'the blades. As a result, so-called pinheads'of clay in the'slip are normally only about 1% of the solids, which is less than in other types of 'blungers Coarse non-clay impurities may occasionally run as `high as 'l0-15%. The lpinheads and coarse impurities areflate'r removed from theslip in a sand classifier.
The relatively la'rge screen openings `serve to prevent any 'large build-up'of impurities, such as sand and quartz, in the' blunger chamber.
EThe flow of clay yand 'water is coordinated so that the slip delivered from the blun'ger chamber 17 hasa solids content (m40-451%, although 50% is perfectly satisfactory. Likewise, vthe`rate of clay feed and rate of water feed are controlled so that the slip, consisting only of "fully disintegrated, or blunged, clay and water, may pass upwardly out of the disintegrating z-one in the lower portion of the blunge'r-chamber 17, the slip passing outwardly through the s'creen53 and-into the Weir 52 for discharge by way of the surge' tank 55.
.The foregoing detailed description is given for clearvness of understanding 4only and no unnecessary limitations are to be understood therefrom, -as some modifications will `be `obvious to those skilled in the art.
I claim:
l1. 'Apparatus for forming clay slip comprising: a chamber; means for feeding clay'into said chamber; means Vfor feeding water into said chamber; means for feeding a dispersing agent `into-*said chamber; a rapidly rotatable headY in said .chamber having a .plurality -of cutter arms, eachof said arms vhavingA a generally horizontally disposed 'cuttingblade with a sharpened forward edge and an uprightl bladefat its -end which is disposed at a small angle Ttoa-line tangent to theiend -of'the arm, said upright blade havinga sharpened forward edgewhich lies inside said line; `and means for withdrawing clay slip from the top `ofsaid chamber. i
2. The apparatus of claim 1 inwhich the cutting edges of said horizontally disposed cutting blades are at the lowerfaces vthereof and `thecutting edges of the upright Ablades are atthe outer` faces of -said blades.
3. Apparatus for forming clay slip comprising: a chamber; a hopper-'through -whichfraw -clay may `be fed into said chamber fromfaboveya conduit for feeding water .and a dispersing agent into-said chamber from below;
an upright, rapidly rotatable spindle in said chamber; a :head -onsaid spindle having a plurality of arms each of which has a generallyhorizontally disposed web blade :and an-.u'prightvblade at itslend, said-*blades having sharpenedfforward edges; a peripheral disposed, foraminous screen at the top of the chamber to .permit the passage l`only fof clay `particles smaller than `a predetermined size;
and a discharge weir surrounding said screen whereby ,said apparatusmayoperate continuously with only fully dispersed clay slip discharging into said Weir.
4. @Apparatus for forming :clay slip comprising: a chamber having a 'generallycylindricalside wall; a hopper through which raw clay may be fed into said chamber from above; a conduit for feeding water and a dispersing agent into said chamber from below; an upright, rapidly rotatable spindle in said chamber; a head on said spindle having a plurality of arms adjacent the bottom of the chamber, each of said arms having a generally horizontally disposed cutting blade and an upright blade at its end, said blades having sharpened forward edges, rotation of said arms producing a rolling, vortex action of the slip in the chamber so that slip adjacent the wal-l of the chamber impinges on the wall at asmall angle and slip near the top of the chamber away from the wall is drawn inwardly and down through the arms; a peripherally disposed, foraminous screen in the wall of the chamber substantially above said arms to permit the passage only of solid particles smaller than a predetermined size, the angular impingement of slip flow on said screen being such that the great majority of particles passing through the screen are only a fraction of the size of the screen opening; and a discharge weir surrounding said screen, whereby said apparatus may operate continuously with only fully dispersed clay slip discharging into said Weir.
5. The apparatus set forth in claim 3 wherein said chamber is substantially cylindrical in shape. j
6. In an apparatus adapted to form clay slip and the like comprising a chamber wherein a disintegrator head assembly is adapted to rapid-ly rotate about a vertical axis, the improvement comprising: a disintegrator head assembly having a Iplurality of horizontally disposed cutting arms provided with blades having forwardly facingshearing type cutting edges, upright blades placed at the outer end of said arms which are inclined with their forward end inwardly from a line tangent to the end of the arm.
7. The apparatus as set forth in claim 6 in which the upright blade has about three-fourths of its height above the horizontally disposed cutting blade.
8. The apparatus set forth in claim 7 in which the upright blade is disposed `at an angle of at least about 8 to the tangent line.
9. The apparatus set forth in claim 8 in which the front edge of the horizontally disposed cutting blades are disposed at an angle of about 120 to the associated upright blade and has its outer end slightly to the rear of the forward edge of said upright blade.
10. Apparatus for forming a clay slip comprising a chamber, a hopper above said chamber through which raw clay may be fed into the chamber, -means for feeding water into the chamber from below, means for feeding a dispersing agent into the chamber, an upright rapidly rotatable spindle in said chamber, drive means for the spindle, a head on said spindle having a plurality of arms having generally horizontally disposed blades and upright cutting blades at the end thereof, a foraminous screen at the top of the chamber to permit the passage only of clay particles smaller than a predetermined size; and a discharge Weir surrounding said screen whereby said apparatus may operate continuously with only dispersed clay slip discharging into said weir.
11. Apparatus for forming clay slip comprising: a chamber; means through which raw clay may be fed into said chamber, means through which a counter ow of water may be fed into said chamber, and means through which a dispersing agent may be fed into said chamber; a rapidly rotatable head adapted to rotate about its vertical axis in saidchamber having a plurality of cutter arms provided with blades having forwardly facing cutting edges so that when said head is rotated the mixture is violently agitated with a vortex action and the clay is subjected to a shearing type of cutting action, each of said cutter arms having a horizontally disposed cutting blade and a straight upright blade at its outer end which is inclined with its forward cutting edge inwardly from a line tangent to the end of said arms; and means for withdrawing clay slip from the top of said chamber.
12. The apparatus as set forth in claim 11 in which the upright blades have 3/4 of their height above the horizontally disposed cutting blades.
t 13. The apparatus of claim 12 in which the upright blades are disposed at an angle of at least about 8 to the tangent line.
14. The apparatus of claim 13 in which the front edge of said horizontally disposed cutting blades are disposed at an angle of about to the associated upright blades and have their outer ends slightly to the rear of said edge of said upright blades.
15. The apparatus for forming clap slip comprising: a chamber; means through which raw clay may be fed into said chamber, means through which a counter-flow of water may be fed into said chamber, and means through which a dispersing agent may be fed into said chamber; a rapidly rotatable head adapted to rotate about its vertical axis in said chamber having a plurality of cutter arms provided with blades having forwardly facing cutting edges so that when said head is rotated the mixture is violently agitated with a vortex action and the clay is subjected to a shearing type of action, each of said cutter arms having an upright blade at its outerend, said upright blades being inclined with their forward cutting edge inwardly from a line tangent to the end of the arms; and means for withdrawing clay slip from the top of said chamber.
16. In an apparatus adapted to form clay slip and the lik-e comprising a chamber wherein a disintegrator head assembly is adapted to rapidly rotate about a vertical axis, the improvement comprising a disintegrator head assembly having a plurality of cutter arms provided with blades having forwardly facing cutting edges, said cutter arms having a horizontally disposed forward cutting blade and an upright blade at its outer end, said upright blade being inclined with its forward cutting edge inwardly from a line tangent to the end of said arms.
References Cited in the le of this patent UNITED STATES PATENTS 2,297,009 Mead et al. Sept. 29, 1942 2,440,601 Dickerman Apr. 27, 1948 2,520,320 Lyons et al Aug. 29, 1950 2,577,353 Naidu et al Dec. 4, 1951 2,665,853 Nicholson Jan. 12, 1954
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Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2916214A (en) * 1957-07-10 1959-12-08 Georgia Kaolin Co Method of blunging clay
US3075710A (en) * 1960-07-18 1963-01-29 Ignatz L Feld Process for wet grinding solids to extreme fineness
US3096034A (en) * 1960-12-28 1963-07-02 Wintershall Ag Method and apparatus for purifying potassium salt-containing materials
US3191872A (en) * 1958-03-03 1965-06-29 Howard W Dyson Disintegrating apparatus
US3455516A (en) * 1967-01-11 1969-07-15 Beloit Corp Pulper
US5366168A (en) * 1993-10-04 1994-11-22 Dymarkowski Paul F Yard waste liquefier

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2297009A (en) * 1940-12-17 1942-09-29 American Cyanamid Co Disintegrating apparatus
US2440601A (en) * 1946-11-14 1948-04-27 Cons Water Power And Paper Com Production of clay suspensions
US2520320A (en) * 1945-09-27 1950-08-29 Georgia Kaolin Co Process and apparatus for winning kaolin and the like
US2577353A (en) * 1948-07-07 1951-12-04 Abbott Lab Process for producing fibrin from whole blood
US2665853A (en) * 1951-08-23 1954-01-12 Black Clawson Co Toothed cutting impeller for pulping solid materials in liquid suspension

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2297009A (en) * 1940-12-17 1942-09-29 American Cyanamid Co Disintegrating apparatus
US2520320A (en) * 1945-09-27 1950-08-29 Georgia Kaolin Co Process and apparatus for winning kaolin and the like
US2440601A (en) * 1946-11-14 1948-04-27 Cons Water Power And Paper Com Production of clay suspensions
US2577353A (en) * 1948-07-07 1951-12-04 Abbott Lab Process for producing fibrin from whole blood
US2665853A (en) * 1951-08-23 1954-01-12 Black Clawson Co Toothed cutting impeller for pulping solid materials in liquid suspension

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2916214A (en) * 1957-07-10 1959-12-08 Georgia Kaolin Co Method of blunging clay
US3191872A (en) * 1958-03-03 1965-06-29 Howard W Dyson Disintegrating apparatus
US3075710A (en) * 1960-07-18 1963-01-29 Ignatz L Feld Process for wet grinding solids to extreme fineness
US3096034A (en) * 1960-12-28 1963-07-02 Wintershall Ag Method and apparatus for purifying potassium salt-containing materials
US3455516A (en) * 1967-01-11 1969-07-15 Beloit Corp Pulper
US5366168A (en) * 1993-10-04 1994-11-22 Dymarkowski Paul F Yard waste liquefier

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